WO2011005463A3 - Membrane haute température sélective à la vapeur d'eau - Google Patents

Membrane haute température sélective à la vapeur d'eau Download PDF

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Publication number
WO2011005463A3
WO2011005463A3 PCT/US2010/039251 US2010039251W WO2011005463A3 WO 2011005463 A3 WO2011005463 A3 WO 2011005463A3 US 2010039251 W US2010039251 W US 2010039251W WO 2011005463 A3 WO2011005463 A3 WO 2011005463A3
Authority
WO
WIPO (PCT)
Prior art keywords
steam
polymer layer
temperature
porous layers
rigid porous
Prior art date
Application number
PCT/US2010/039251
Other languages
English (en)
Other versions
WO2011005463A2 (fr
Inventor
Ashok Joshi
Original Assignee
Ceramatec, Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Ceramatec, Inc filed Critical Ceramatec, Inc
Priority to EP10797535.1A priority Critical patent/EP2445617A4/fr
Publication of WO2011005463A2 publication Critical patent/WO2011005463A2/fr
Publication of WO2011005463A3 publication Critical patent/WO2011005463A3/fr

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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/26—Drying gases or vapours
    • B01D53/268—Drying gases or vapours by diffusion
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/22—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/22—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion
    • B01D53/228—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion characterised by specific membranes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/10—Supported membranes; Membrane supports
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/12—Composite membranes; Ultra-thin membranes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/12—Composite membranes; Ultra-thin membranes
    • B01D69/1213—Laminated layers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/14—Dynamic membranes
    • B01D69/141—Heterogeneous membranes, e.g. containing dispersed material; Mixed matrix membranes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/02—Inorganic material
    • B01D71/024—Oxides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06—Organic material
    • B01D71/52—Polyethers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06—Organic material
    • B01D71/52—Polyethers
    • B01D71/522—Aromatic polyethers
    • B01D71/5222—Polyetherketone, polyetheretherketone, or polyaryletherketone
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06—Organic material
    • B01D71/76—Macromolecular material not specifically provided for in a single one of groups B01D71/08 - B01D71/74
    • B01D71/82—Macromolecular material not specifically provided for in a single one of groups B01D71/08 - B01D71/74 characterised by the presence of specified groups, e.g. introduced by chemical after-treatment
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2313/00—Details relating to membrane modules or apparatus
    • B01D2313/42—Catalysts within the flow path

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Dispersion Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

L'invention porte sur une membrane haute température sélective à la vapeur d'eau (100) destinée à ajouter de la vapeur d'eau à divers types de réactions chimiques ou à enlever de la vapeur d'eau de ceux-ci. Dans un mode de réalisation, une telle membrane comprend une couche de polymère (102) présentant une sélectivité élevée pour le transport de vapeur d'eau par rapport à d'autres espèces gazeuses. La couche de polymère (102) est prise en sandwich entre des couches poreuses pratiquement rigide (104a et 104b) qui sont perméables à la vapeur d'eau. Les couches poreuses rigides (104a et 104b) immobilisent pratiquement la couche de polymère (102) et réduisent la tendance de la couche de polymère (102) à rétrécir et/ou se dilater en réponse à des variations de température ou d'humidité. Les couches poreuses rigides (104a et 104b) peuvent également retenir l'eau pour maintenir la couche de polymère (102) humide. Le support physique et la rétention d'humidité fournis par les couches poreuses rigides (104a et 104b) permettent à la couche de polymère (102) de fonctionner sur une plage de température d'environ 100°C à 500°C.
PCT/US2010/039251 2009-06-23 2010-06-18 Membrane haute température sélective à la vapeur d'eau WO2011005463A2 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP10797535.1A EP2445617A4 (fr) 2009-06-23 2010-06-18 Membrane haute température sélective à la vapeur d'eau

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US21956409P 2009-06-23 2009-06-23
US61/219,564 2009-06-23

Publications (2)

Publication Number Publication Date
WO2011005463A2 WO2011005463A2 (fr) 2011-01-13
WO2011005463A3 true WO2011005463A3 (fr) 2011-04-21

Family

ID=43353152

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US2010/039251 WO2011005463A2 (fr) 2009-06-23 2010-06-18 Membrane haute température sélective à la vapeur d'eau

Country Status (3)

Country Link
US (1) US20100319535A1 (fr)
EP (1) EP2445617A4 (fr)
WO (1) WO2011005463A2 (fr)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013044168A1 (fr) 2011-09-22 2013-03-28 Chevron U.S.A. Inc. Appareil et procédé de traitement de l'eau
US8870735B2 (en) 2012-05-17 2014-10-28 Strategic Environmental & Energy Resources, Inc. Waste disposal
GB201211309D0 (en) 2012-06-26 2012-08-08 Fujifilm Mfg Europe Bv Process for preparing membranes
RS59961B1 (sr) * 2014-06-16 2020-03-31 Core Energy Recovery Solutions Inc Mešovite membrane za transport vodene pare i postupci za izradu istih
EP3169987A1 (fr) * 2014-07-18 2017-05-24 THE UNITED STATES OF AMERICA, represented by the S Systèmes de croissance de particules d'aérosol à l'aide de membranes à électrolyte polymère
US9932257B2 (en) 2016-07-29 2018-04-03 Chevron U.S.A. Inc. Systems and methods for producing regenerant brine and desalinated water from high temperature produced water
EP3788304B1 (fr) * 2018-05-04 2023-08-09 Donaldson Company, Inc. Systèmes et procédés destinés à éliminer des composés organiques présents dans de la vapeur
US10639591B1 (en) * 2019-01-07 2020-05-05 Compact Membrane Systems, Inc. Thin-film composite membrane and processes for the separation of alkenes from a gaseous feed mixture
US11649178B2 (en) 2019-10-15 2023-05-16 Donaldson Company, Inc. Systems and methods for removing organic compounds from water used to generate steam
CN114432902B (zh) * 2020-11-05 2023-03-14 中国石油化工股份有限公司 一种复合纳滤膜及其制备方法和应用

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60261503A (ja) * 1984-06-08 1985-12-24 Sumitomo Electric Ind Ltd 水蒸気分離膜及びその製造方法
US5229102A (en) * 1989-11-13 1993-07-20 Medalert, Inc. Catalytic ceramic membrane steam-hydrocarbon reformer
US5888605A (en) * 1995-10-31 1999-03-30 Nitto Denko Corporation Polysulfone semipermeable membrane and method of manufacturing the same
US20020014154A1 (en) * 1996-09-27 2002-02-07 Richard Witzko Separation of gaseous components from a gas stream with a liquid absorbent

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US4751104A (en) * 1984-12-06 1988-06-14 Uop Inc. Preparation of gas selective membranes
EP0284052B1 (fr) * 1987-03-25 1993-09-29 Hitachi, Ltd. Procédé pour la production d'eau ultrapure et pour l'utilisation de cette eau
EP0326083B1 (fr) * 1988-01-26 1994-06-01 Asahi Glass Company Ltd. Membrane permseléctif de vapeur
JPH01194927A (ja) * 1988-01-27 1989-08-04 Japan Gore Tex Inc 水蒸気選択透過膜
JP3213430B2 (ja) * 1993-03-31 2001-10-02 日本碍子株式会社 ガス分離体及びその製造方法
US6048383A (en) * 1998-10-08 2000-04-11 International Fuel Cells, L.L.C. Mass transfer composite membrane for a fuel cell power plant
US6635104B2 (en) * 2000-11-13 2003-10-21 Mcmaster University Gas separation device
US20070022877A1 (en) * 2002-04-10 2007-02-01 Eva Marand Ordered mesopore silica mixed matrix membranes, and production methods for making ordered mesopore silica mixed matric membranes
US7789930B2 (en) * 2006-11-13 2010-09-07 Research Triangle Institute Particle filter system incorporating nanofibers
DE112005001084B4 (de) * 2004-05-18 2008-07-10 Asahi Kasei Kabushiki Kaisha Gasseparator und Verfahren zu dessen Betrieb
US7753991B2 (en) * 2004-07-30 2010-07-13 Kertzman Systems, Inc. Water transport method and assembly including a thin film membrane for the addition or removal of water from gases or liquids
US7559979B2 (en) * 2005-02-04 2009-07-14 Ngk Insulators, Ltd. Hydrogen separator and method for production thereof
WO2007058698A2 (fr) * 2005-09-13 2007-05-24 Rasirc Procede de production de vapeur a haute purete
US9203098B2 (en) * 2005-10-26 2015-12-01 Nanotek Instruments, Inc. Organic vapor fuel cell
EP1966307A4 (fr) * 2005-12-28 2011-06-22 Coorstek Inc Recuperation de vapeur d'eau au moyen d'une membrane conductrice d'ions mixtes permeable a la vapeur d'eau
EP1921702A1 (fr) * 2006-11-10 2008-05-14 DSMIP Assets B.V. Membrane d'humidificateur
AU2009230868A1 (en) * 2008-03-31 2009-10-08 Commonwealth Scientific And Industrial Research Organisation Membrane and process for steam separation, purification and recovery

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60261503A (ja) * 1984-06-08 1985-12-24 Sumitomo Electric Ind Ltd 水蒸気分離膜及びその製造方法
US5229102A (en) * 1989-11-13 1993-07-20 Medalert, Inc. Catalytic ceramic membrane steam-hydrocarbon reformer
US5888605A (en) * 1995-10-31 1999-03-30 Nitto Denko Corporation Polysulfone semipermeable membrane and method of manufacturing the same
US20020014154A1 (en) * 1996-09-27 2002-02-07 Richard Witzko Separation of gaseous components from a gas stream with a liquid absorbent

Also Published As

Publication number Publication date
EP2445617A4 (fr) 2014-07-02
US20100319535A1 (en) 2010-12-23
EP2445617A2 (fr) 2012-05-02
WO2011005463A2 (fr) 2011-01-13

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